Difference between revisions of "Team:Amsterdam/Project/Eng rom/Photosyn car"
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− | In an attempt to further increase acetate production and increase the production capacity of our consortium, we took the acs mutant described above and over-expressed the ackA1 gene and pta gene - encoding the two reactions that lead to acetate formation in the biomass formation pathway. During the engineering of the pta strain, we discovered several mutations had occurred in pta fragment, resulting in a frame-shift mutation that removed the stop codon and extended the amino acid chain. We therefore created a second strain from scratch, but included the first strain to investigate the impact of the frameshift mutations. The three resulting strains, ackA1, pta mutated, and pta, were cultivated in a photostat, a batch reactor with OD-dependent light intensity, over a period of four days with samples taken every four hours until an OD treshold was reached. The results shown in figure 6 and 7 show that although overall acetate concentrations were higher in the pta strain (again, this also has the acs KO background) compared to the acs mutant strain, the average Q<sub>p</sub>'s are higher for the acs mutant. These results suggest that over-expressing ackA1 or pta does not result in increased acetate production | + | In an attempt to further increase acetate production and increase the production capacity of our consortium, we took the acs mutant described above and over-expressed the ackA1 gene and pta gene - encoding the two reactions that lead to acetate formation in the biomass formation pathway. During the engineering of the pta strain, we discovered several mutations had occurred in pta fragment, resulting in a frame-shift mutation that removed the stop codon and extended the amino acid chain. We therefore created a second strain from scratch, but included the first strain to investigate the impact of the frameshift mutations. The three resulting strains, ackA1, pta mutated, and pta, were cultivated in a photostat, a batch reactor with OD-dependent light intensity, over a period of four days with samples taken every four hours until an OD treshold was reached. The results shown in figure 6 and 7 show that although overall acetate concentrations were higher in the pta strain (again, this also has the acs KO background) compared to the acs mutant strain, the average Q<sub>p</sub>'s are higher for the acs mutant. These results suggest that over-expressing ackA1 or pta does not result in increased acetate production and may in fact decrease it. Exploring other strategies to further increase acetate production would be the first thing on our agenda if we were to continue this research. |
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Revision as of 23:28, 18 September 2015
Engineering Stable Carbon Production
Sharing is Caring
Overview
Background
The driving force of our consortium's romance is the phototrophic carbon-sharing module: an engineered Synechocystis that fixates CO2 and produces compounds that can be used by a chemotroph to create desired end-products like biofuels.
Aim
Productive relationships need to stand the test of time. Having experienced the perils of instability firsthand, we sought to engineer carbon production in way that would last.
Approach
Using genetic engineering strategies guided by modelling results, we used a combination of gene knock-outs and over-expressions to target a pathway that would result in growth-coupled acetate production.
Results
- We engineered growth-coupled acetate production by knocking out the acs gene, showing that this indeed leads to stable acetate production
- We over-expressed the Pta and AckA1 genes to increase the flux towards acetate formation.
Connections
- Stable Romance: Measure stability.
- Engineering Romance: Estimate parameters of new strains.
- Simulating Romance: Provide parameters.
Change of plans
Different carbon compounds produced by Synechocystis could serve as fuel for E. coli in our consortium: Glucose, lactate, and glycerol for example, are all products that an engineered cyanobacteria can produce.
Although glucose seems like a great compound to drive sustainable bio-production with, our initial plan was to develop Synechocystis strains that produce all of these products, and to compare their performances in a consortium with E. coli generating different products. After the initial results of lactase production came in, however, we decided to make genetic stability the central focus of our carbon fixation efforts: engineering a Synechocystis that produces a carbon compound in the most stable way possible such that its relationships with other consortia-species last more than one or a few nights. Based on the results of our software tools, which parsed the genome-scale metabolic map to search for compounds that could be produced in a growth-coupled way, we decided to engineer acetate production.
Methods
As the genetic engineering of carbon production in Synechocystis involved relatively simple constructs, standard restriction-digestion cloning protocols were used for most engineering efforts. Synechocystis knock-outs were created using the specific markerless knock-out method described by [ref]. This two-round knock-out approach allowed for the cultivation of knock-out strains without the need of antibiotics and thus increased flexibility of implementation in a potential consortium.
Acetate production involved the knock-out of the native acs gene and heterologous over-expression of the ackA1 gene from Lactocuccus lactis and pta gene from Synechocystis.
The acs gene codes for acetyl-CoA synthase, an enzyme that converts acetate into acetyl CoA. This is the acetate recycling reaction in the biomass formation pathway. The reactions that actually lead to the formation of acetate as a side-product represent a two-step process and are governed by pta, coding for the phosphate acetyl-transferase enzyme that converts acetyl-CoA into acetyl-phosphate, and ack, coding for an acetate kinase that removes acetyl-phosphate's phosphate group to produce acetate (technically functioning as a phosphatase). Although over-expressing ackA1 and pta via gene insertions is prone to fixating mutations, we still wanted to see its impact on overall acetate production. The following constructs were used for the knocking out of acs and insertion of ackA1, pta, or fused AckA1/pta:
After the genetic engineering steps, batch and turbidostat cultivation experiments were conducted to measure acetate production and stability. Acetate concentrations were measured using the Megazyme acetate assay kit.
Results
Stable acetate production
By knocking out the acs gene, we expected to eliminate the acetate recycling reaction in the biomass formation pathway, which would lead to acetate accumulation in growth-coupled fashion. Although this is what the model indicated should happen, modelling results hardly ever translate perfectly to real-world scenarios. In order to test the Synechocystis acs mutant's acetate production (only acs was knocked out for this strain, ack and pta were not yet overexpressed), we conducted the turbidostat experiments described in more detail on this page.
We indeed observed stable acetate production over time, maintained well over 900 hours until the end of the experiment. The contrast this result offers to the lactate results shows that knocking out the acetate recycling reaction in the biomass-formation pathway represents a succesful strategy for inducing stable production.
Ramping up production
In an attempt to further increase acetate production and increase the production capacity of our consortium, we took the acs mutant described above and over-expressed the ackA1 gene and pta gene - encoding the two reactions that lead to acetate formation in the biomass formation pathway. During the engineering of the pta strain, we discovered several mutations had occurred in pta fragment, resulting in a frame-shift mutation that removed the stop codon and extended the amino acid chain. We therefore created a second strain from scratch, but included the first strain to investigate the impact of the frameshift mutations. The three resulting strains, ackA1, pta mutated, and pta, were cultivated in a photostat, a batch reactor with OD-dependent light intensity, over a period of four days with samples taken every four hours until an OD treshold was reached. The results shown in figure 6 and 7 show that although overall acetate concentrations were higher in the pta strain (again, this also has the acs KO background) compared to the acs mutant strain, the average Qp's are higher for the acs mutant. These results suggest that over-expressing ackA1 or pta does not result in increased acetate production and may in fact decrease it. Exploring other strategies to further increase acetate production would be the first thing on our agenda if we were to continue this research.